Effect of the ionizing radiation on the catalytic activity of the BASF K-3-10 catalyst in the low-temperature conversion of carbon monoxide by water vapour. Catalytic activity of the pre-irradiated catalyst

1986 ◽  
Vol 51 (2) ◽  
pp. 279-287 ◽  
Author(s):  
Alois Motl

The catalytic activity of the BASF K-3-10 catalyst with regard to the low-temperature conversion of carbon monoxide by water vapour and its changes after irradiation of the contact area by gamma or beta radiation or by fast neutrons has been investigated. The irradiated samples exhibit a moderately or even substantially higher catalytic activity in comparison with the non-irradiated catalyst, the change being dependent on the absorbed dose; moreover, the effective activation energy of the reaction increases, too. Important differences in the action of different types of the ionizing radiation used have been observed and their probable explanation is offered. In course of these experiments the catalysts were analyzed and the specific surface of the catalyst was measured at various stages of their history. It has been found that at all stages the specific surfaces of the irradiated catalyst are equal to the respective specific surfaces of the non-irradiated contacts.

1986 ◽  
Vol 51 (8) ◽  
pp. 1571-1578 ◽  
Author(s):  
Alois Motl

The radiation catalytic properties of the BASF K-3-10 catalyst were studied, namely the dependence of these effects on the time interval between the catalyst irradiation and the reaction itself and also on the length of the catalyst use. The catalytic effects decrease exponentially with the interval between the irradiation and the reaction if the catalyst is kept in the presence of air. The stability of effects induced by various types of radiations increases in the sequence beta radiation - gamma radiation - fast neutrons. The radiation catalytic effect stability in the reaction increases in the same sequence.


1989 ◽  
Vol 54 (8) ◽  
pp. 2083-2090
Author(s):  
Alois Motl

The catalytical activity of the BASF K-3-10 catalyst for the low-temperature conversion of carbon monoxide by water vapour has been studied in dependence on the activity of incorporated radionuclide 32P. Radioactivity of the catalytical bed ranged from 0 to 630 MBq of incorporated 32P. It has been observed that at first the catalytical activity increases with the increasing activity of 32P and finally it reaches a limit value that is by about 50 per cent higher than that of the same non-radioactive catalyst. The comparison of these results with those obtained in the studies of the catalytical activity of the same catalyst pre-irradiated by β radiation of the 90Sr-90Y source revealed that in the case of radioactive beds the observed positive radiation-catalytical effect can be ascribed to the pre-irradiation of the catalyst (during the period between the preparation of the radioactive catalytical bed and the catalytical reduction itself) and to the interactions of the ionizing radiation with the catalyst during the subsequent operations. The radiation-catalytical effects induced by the two processes mentioned above differ substantially by their time stability. The probable explanation of the nature of these two effects is proposed using the published mechanism of this reaction.


1980 ◽  
Vol 45 (3) ◽  
pp. 783-790 ◽  
Author(s):  
Petr Taras ◽  
Milan Pospíšil

Catalytic activity of nickel-molybdenum catalysts for methanation of carbon monoxide and hydrogen was studied by means of differential scanning calorimetry. The activity of NiMoOx systems exceeds that of carrier-free nickel if x < 2, and is conditioned by the oxidation degree of molybdenum, changing in dependence on the composition in the region Mo-MoO2. The activity of the catalysts is adversely affected by irradiation by fast neutrons, dose 28.1 Gy, or by γ rays using doses in the region 0.8-52 kGy. The system is most susceptible to irradiation in the region of low concentrations of the minor component (about 1 mol.%). The dependence of changes in catalytic activity of γ-irradiated samples on the dose exhibits a maximum in the range of 2-5 kGy. The changes in catalytic activity are stimulated by the change of reactivity of the starting mixed oxides, leading to different kinetics of their reduction and modification of their adsorption properties. The irradiation of the catalysts results in lowered concentration of the active centres for the methanation reaction.


Implicit solutions of the time-dependent flame equations have been used to calculate, for assumed reaction mechanisms, the expected structures and properties of a series of hydrogen-carbon monoxide-oxygen-nitrogen flames, some containing traces of added water vapour, at atmospheric and reduced pressures. Predicted burning velocities at atmospheric pressure have been compared with: ( a ) recent measurements, reported here, of the effect of addition of up to 10 % carbon monoxide on the burning velocity of a low temperature hydrogen-oxygennitrogen flame; ( b ) previous measurements by Scholte & Vaags (1959c) on dry hydrogen-carbon monoxide-air mixtures over the whole composition range on the fuel-rich side of stoichiometric; and ( c ) previously reported measurements by Jahn (1934), Badami & Egerton (1955), Scholte & Vaags (1959 b )and Wires et al . (1959) for moist carbon monoxide-air or carbon monoxide-oxygen mixtures, with or without traces of added hydrogen. Additionally, the following comparisons are made: ( d )The mole fraction profile for the decay of a trace of carbon dioxide added to the low temperature hydrogen-oxygen-nitrogen flame has been recalculated with the aid of the full reaction mechanism, for comparison with the previously reported measurements of Dixon-Lewis et al. (1965). ( e ) Computed structures of two hydrogen-carbon monoxide-oxygen-argon flames burning at reduced pressure have been compared with previous measurements by Fenimore & Jones (1959) and Vandooren et al . (1975). ( f ) The mole fraction ratio X co /X CO 2 in the burnt gas from a low temperature, fuel-rich hydrogen-carbon monoxide-oxygen-argon flame at atmospheric pressure was measured by using a mass spectrometer. The measured ratio agreed to within 1 % with that predicted by computation of the complete flame properties. Both the calculated and measured ratios were higher than would correspond with the establishment of the water gas equilibrium in the flame. The major part of the observed changes in burning velocity from those of hydrogen-air mixtures can be satisfactorily explained by the addition of the single reaction (xxi) , OH + CO ⇌ C O 2 + H , ( xxi ) to the mechanism already established for the hydrogen-oxygen-nitrogen flame system (Dixon-Lewis 1979). This applies particularly to fuel-lean flames and to fuel-rich mixtures not too far from stoichiometric. For fuel-rich flames further from stoichiometric, and particularly for the measurements in §(a), agreement between predicted and measured burning velocities is improved by adding to the mechanism a series of chain terminating steps involving the formation and subsequent reactions of the formyl radical. For reasonable values of its rate coefficient, reaction (xxii), O + CO + M ⇌ C O 2 + M , ( xxii ) never exerts more than a minor influence on the burning velocity. The major features of the structure of the flames are: ( a ) a preferential oxidation of hydrogen in the early stages of the reaction zones, leading to overshoot in the water concentration followed by a slow approach to the water gas equilibrium from the carbon monoxide-water side; and ( b ) marked enrichment of the oxygen atom concentration in the radical pool as the hydrogen content of the flames is decreased. In the flames containing only traces of hydrogen, the degree of enrichment is markedly influenced by reaction (xxii).


RSC Advances ◽  
2016 ◽  
Vol 6 (79) ◽  
pp. 75126-75132 ◽  
Author(s):  
Weining Zhang ◽  
Qingguo Zhao ◽  
Xiaohong Wang ◽  
Xiaoxia Yan ◽  
Sheng Han ◽  
...  

Au@CuxO core–shell nanoparticles and Au@CuxO/Al2O3 used for CO oxidation at low temperature are prepared. CO conversion on Au@CuxO/Al2O3 can reach to 38% at room temperature and the catalytic activity remains unchanged after 108 hours reaction.


2018 ◽  
Vol 52 (4) ◽  
pp. 307-311
Author(s):  
E. Yu. Liberman ◽  
A. V. Naumkin ◽  
A. A. Revina ◽  
A. I. Mikhailichenko ◽  
M. V. Tsodikov ◽  
...  

1987 ◽  
Vol 52 (10) ◽  
pp. 2383-2391 ◽  
Author(s):  
Alois Motl

The effects of various thermal treatment methods on the radiation catalytical effects, induced by the pre-irradiation of the BASF K-3-10 catalyst by the γ- or β-radiation or by fast neutrons, were investigated. It has been found that the calcination of the irradiated non-reduced catalyst results in a strong decrease or even in total disappearance of the final radiation catalytical effects; however, at the same time the catalytical activity of the unirradiated catalyst was found to increase. The calcination of the catalysts in nitrogen atmosphere after reduction led also to a substantial decrease of the resulting positive radiation catalytical effects and exceeding a certain calcination temperature resulted in the decrease even of the unirradiated catalyst activity. It could be concluded that the calcination in nitrogen of the reduced irradiated samples decreases the radiation catalytical effects less than the calcination on air of the non-reduced irradiated samples. In both cases a different thermal stability of effects induced by different types of the ionizing radiation has been observed and it has been found that it increases in the sequence beta radiation – gamma radiation – fast neutrons. The investigation of the γ radiation dose dependence of the radiation catalytical effect on the catlyst calcinated before irradiation under the access of air showed that the final radiation catalytical effects are lower than those observed in the case of similarly irradiated but non-calcinated samples. At the same time the dose dependence of the effect has the same character in both cases.


Catalysts ◽  
2021 ◽  
Vol 11 (12) ◽  
pp. 1480
Author(s):  
Pavel Straka ◽  
Olga Bičáková ◽  
Tomáš Hlinčík

A thermal conversion of biomass to hythane using catalysts was studied. Low-temperature pyrolysis of two different types of biomass was performed in a pressure sealed reactor, and the resulting gas with high contents of CO2 and CO was methanized in a hydrogen atmosphere at a pressure of 30 bar. As catalysts, Ni/Al2O3, NiCo/Al2O3 and NiMo/Al2O3 were used and their catalytic activity was evaluated. The NiCo/Al2O3 catalyst showed the highest catalytic activity, Ni/Al2O3 had a lower but comparable one, and NiMo/Al2O3 showed the lowest activity. The resulting hythane contained 70 vol.% CH4 and 10 vol.% H2 (with NiCo/Al2O3 catalyst, HHV 29.20 MJ/m3, LHV 26.32 MJ/m3), or 57 vol.% CH4 and 23 vol% H2 (with Ni/Al2O3, HHV 25.92 MJ/m3, LHV 23.21 MJ/m3) or 47 vol.% CH4 and 27 vol.% H2 (with NiMo/Al2O3, HHV 23.23 MJ/m3, LHV 20.76 MJ/m3). It has been found that secondary reactions of volatile biomass products are of great importance for successful pressure pyrolysis.


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